Catalysts and Methods for Complex Carbohydrate Hydrolysis

a technology of complex carbohydrates and catalysts, which is applied in the direction of physical/chemical process catalysts, sugar derivates, organic chemistry, etc., can solve the problems of complex carbohydrates that are not readily metabolized, not as readily usable by living organisms as glucose, and create safety problems

Inactive Publication Date: 2008-08-14
SARTEC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, most complex carbohydrates are not as readily usable by living organisms as glucose.
These polysaccharides are largely insoluble in water and are not readily metabolized by most organisms without reduction to simpler sugars.
Unfortunately, strong acids are usually highly caustic and can create safety issues.
In addition, recovery of the acid after the reaction makes this approach relatively costly and time consuming.
Unfortunately, these enzymatic reactions generally take a significant amount of time to reach completion.
In addition, because the enzymes are proteins, they are subject to denaturation (wherein they lose their enzymatic capability) and are relatively fragile (chemically and thermally), constraining the possible reaction conditions.
Finally, enzymes are relatively expensive to produce.

Method used

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  • Catalysts and Methods for Complex Carbohydrate Hydrolysis
  • Catalysts and Methods for Complex Carbohydrate Hydrolysis
  • Catalysts and Methods for Complex Carbohydrate Hydrolysis

Examples

Experimental program
Comparison scheme
Effect test

example 1

Formation of Zirconia Particles

[0063]A colloidal dispersion of zirconium oxide (NYACOL™ ZR 100 / 20) (Nyacol Nano Technologies, Inc., Ashland, Mass.), containing 20 wt. % ZrO2 primarily as about 100 nm particles was spray dried. As the dispersion dried, the particles interacted strongly with one another to provide aggregated ZrO2 particles. The dried aggregated particles that were obtained were examined under an optical microscope and observed to consist mostly of spherules from about 0.5 μm to about 15 μm in diameter.

[0064]The dried spherules were then sintered by heating them in a furnace at a temperature of 750° C. for 6 hours. The spherules were air classified, and the fraction having a size of approximately 10 μm was subsequently isolated. The particles were all washed in sodium hydroxide (1.0 Molar), followed by water, nitric acid (1.0 Molar), water and then dried under vacuum at 110° C. BET nitrogen porosimetry was performed in order to further characterize the sintered spherul...

example 2

Formation of Base Modified Zirconia Particles

[0065]1 liter of 2.0 M sodium hydroxide was placed in a 2 liter plastic Erlenmeyer flask. 110 g of 5-15 μm bare zirconia prepared as described in Example 1 was put into the flask. The particle suspension was sonicated for 10 minutes under vacuum and then swirled for 2 hours at ambient temperature. The particles were then allowed to settle and the alkaline solution was decanted and then 1.4 liters of HPLC-grade water was added to the flask followed by settling and decanting. Then 200 mL of HPLC-grade water was added back to the flask and the particles were collected on a nylon filter with 0.45 micron pores. The collected particles were then washed with 2 aliquots of 200 mL HPLC-grade water followed by 3 aliquots of 200 mL of HPLC-grade methanol. Air was then allowed to pass through the particles until they were free-flowing.

example 3

Formation of a Packed Column

[0066]Particles as formed in Example 3 were slurried in methanol (26 g zirconia in 44 mL of methanol) and packed into a 15 cm×10.0 mm i.d. stainless steel HPLC column at 7,000 PSI using methanol as a pusher solvent. The column was allowed to pack for 8 minutes under pressure and then the pressure was allowed to slowly bleed off and the end fitting and frit were attached to the inlet of the column. 200 mL of total solvent was collected in the packing process.

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Abstract

The present invention relates to methods and catalysts for hydrolyzing complex carbohydrates. In an embodiment, the invention includes a process for producing monosaccharides from a complex carbohydrate feedstock including the operations of heating the complex carbohydrate feedstock to a temperature greater than about 150 degrees Celsius and contacting the complex carbohydrate feedstock with a metal oxide catalyst. In an embodiment, the invention includes a method of hydrolyzing complex carbohydrates including the operations of heating the complex carbohydrate feedstock to a temperature greater than about 150 degrees Celsius and passing the complex carbohydrate feedstock through a housing to form a reaction product mixture. In an embodiment, the invention includes a polysaccharide hydrolysis reactor including a reactor housing and a catalyst disposed within the reactor housing. Other embodiments are also described herein.

Description

[0001]This application claims the benefit of U.S. Provisional Application No. 60 / 889,730, filed Feb. 13, 2007, and U.S. Provisional Application No. 60 / 911,313, filed Apr. 12, 2007, the contents of all of which are herein incorporated by reference in their entirety.FIELD OF THE INVENTION [0002]The present invention relates to methods and catalysts for breaking down carbohydrates. More specifically, the invention relates to methods and catalysts for hydrolyzing complex carbohydrates.BACKGROUND OF THE INVENTION [0003]Carbohydrates are fundamentally important molecules to living organisms. Carbohydrates include a group of organic compounds based on the general formula Cx(H2O)y. The group specifically includes monosaccharides, disaccharides, oligosaccharides, polysaccharides (sometimes called “glycans”), and their derivatives. Some carbohydrates serve as a chemical store of energy for living organisms. For example, glucose is a monosaccharide found in fruits, honey, and the blood of many...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): C07H1/00B01J19/00
CPCC07H3/02C07H1/00
Inventor MCNEFF, LARRY C.
Owner SARTEC
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